NOx ADSORBER CATALYST

Abstract

A method of treating an exhaust gas from an internal combustion engine comprising contacting the exhaust gas with a lean NO.sub.x trap catalyst is disclosed. The lean NO.sub.x trap catalyst comprises a first layer and a second layer.

Claims

1. A method of treating an exhaust gas from an internal combustion engine comprising contacting the exhaust gas with a lean NO.sub.x trap catalyst, the lean NO.sub.x trap catalyst comprising: i) a first layer, said first layer comprising one or more platinum group metals, a first ceria-containing material, and a first inorganic oxide; ii) a second layer, said second layer comprising one or more noble metals, a second ceria-containing material, and a second inorganic oxide; and wherein the first ceria-containing material or the first inorganic oxide comprises a rare earth dopant.

2. The method of claim 1, wherein the rare earth dopant comprises one or more of scandium, yttrium, lanthanum, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, or metal oxides thereof, preferably wherein the rare earth dopant comprises lanthanum, neodymium, or metal oxides thereof, more preferably wherein the rare earth dopant comprises lanthanum.

3. The method of claim 1, wherein the total loading of the one or more platinum group metals in the first layer is lower than the total loading of the one or more noble metals in the second layer, preferably wherein the ratio of the total loading of the one or more noble metals in the second layer to the total loading of the one or more platinum group metals in the first layer is at least 2:1 on a w/w basis.

4. The method of claim 1, wherein the total loading of the first ceria-containing material is greater than the total loading of the second ceria-containing material, preferably wherein the ratio of the total loading of the first ceria-containing material is greater than the total loading of the second ceria-containing material is at least 2:1 on a w/w basis.

5. The method of claim 1, wherein said one or more platinum group metals is selected from the group consisting of palladium, platinum, rhodium, and mixtures thereof, preferably wherein said one or more platinum group metals is a mixture or alloy of platinum and palladium.

6. The method of claim 1, wherein the one or more platinum group metals are supported on the first ceria-containing material.

7. The method of claim 1, wherein said first ceria-containing material is selected from the group consisting of cerium oxide, a ceria-zirconia mixed oxide, and an alumina-ceria-zirconia mixed oxide, preferably wherein the first ceria-containing material comprises bulk ceria.

8. The method of claim 1, wherein the first inorganic oxide is selected from the group consisting of alumina, ceria, magnesia, silica, titania, zirconia, niobia, tantalum oxides, molybdenum oxides, tungsten oxides, and mixed oxides or composite oxides thereof, preferably wherein the first inorganic oxide is alumina, ceria, or a magnesia/alumina composite oxide.

9. The method of claim 1, wherein the one or more noble metals is selected from the group consisting of palladium, platinum, rhodium, silver, gold, and mixtures thereof.

10. The method of claim 1, wherein the one or more noble metals is a mixture or alloy of platinum and palladium, preferably wherein the ratio of platinum to palladium is from 2:1 to 10:1 on a w/w basis, more preferably wherein the ratio of platinum to palladium is about 5:1 on a w/w basis.

11. The method of claim 1, wherein the one or more noble metals are supported on the second ceria-containing material.

12. The method of claim 1, wherein the second inorganic oxide is selected from the group consisting of alumina, ceria, magnesia, silica, titania, zirconia, niobia, tantalum oxides, molybdenum oxides, tungsten oxides, and mixed oxides or composite oxides thereof, preferably wherein the second inorganic oxide is alumina, ceria, or a magnesia/alumina composite oxide, more preferably wherein the second inorganic oxide is alumina.

13. The method of claim 1, wherein said second ceria-containing material is selected from the group consisting of cerium oxide, a ceria-zirconia mixed oxide, and an alumina-ceria-zirconia mixed oxide, preferably wherein the second ceria-containing material comprises bulk ceria.

14. The method of claim 1, wherein the lean NOx trap catalyst further comprises a metal or ceramic substrate having an axial length L, preferably wherein the substrate is a flow-through monolith or a filter monolith, and/or wherein the first layer is supported/deposited directly on the metal or ceramic substrate.

15. The method of claim 1, wherein the second layer is deposited on the first layer.

16. The method of claim 1, wherein the first layer and/or second layer is extruded to form a flow-through or filter substrate.

17. The method of claim 1, wherein the internal combustion engine is a diesel engine and/or wherein the exhaust gas is at a temperature of about 150 to 300° C.

18. The method of claim 1, wherein the exhaust gas cycles between a rich gas mixture and a lean gas mixture.

19. The method of claim 1, wherein said first layer and/or said second layer are substantially free of rhodium.

20. The method of claim 1, wherein said first layer is substantially free of barium.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0022] The lean NO.sub.x trap catalyst of the invention comprises: [0023] i) a first layer, said first layer comprising one or more platinum group metals, a first ceria-containing material, and a first inorganic oxide; [0024] ii) a second layer, said second layer comprising one or more noble metals, a second inorganic oxide, and a second ceria-containing material; and
wherein the first ceria-containing material or the first inorganic oxide comprises a rare earth dopant.

[0025] The one or more platinum group metals is preferably selected from the group consisting of palladium, platinum, rhodium, and mixtures thereof. Particularly preferably, the one or more platinum group metals is a mixture or alloy of platinum and palladium, preferably wherein the ratio of platinum to palladium is from 2:1 to 12:1 on a w/w basis, especially preferably about 5:1 on a w/w basis.

[0026] The lean NO.sub.x trap catalyst preferably comprises 0.1 to 10 weight percent PGM, more preferably 0.5 to 5 weight percent PGM, and most preferably 1 to 3 weight percent PGM. The PGM is preferably present in an amount of 1 to 100 g/ft.sup.3, more preferably 10 to 80 g/ft.sup.3, most preferably 20 to 60 g/ft.sup.3.

[0027] Preferably the one or more platinum group metals do not comprise or consist of rhodium. In other words, the first layer is preferably substantially free of rhodium.

[0028] The one or more platinum group metals are generally in contact with the first ceria-containing material. Preferably the one or more platinum group metals are supported on the first ceria-containing material. Alternatively or additionally, the one or more platinum group metals are supported on the first inorganic oxide.

[0029] The first ceria-containing material is preferably selected from the group consisting of cerium oxide, a ceria-zirconia mixed oxide, and an alumina-ceria-zirconia mixed oxide. Preferably the first ceria-containing material comprises bulk ceria. The first ceria-containing material may function as an oxygen storage material. Alternatively, or in addition, the first ceria-containing material may function as a NO.sub.x storage material, and/or as a support material for the one or more platinum group metals.

[0030] The first inorganic oxide is preferably an oxide of Groups 2, 3, 4, 5, 13 and 14 elements The first inorganic oxide is preferably selected from the group consisting of alumina, ceria, magnesia, silica, titania, zirconia, niobia, tantalum oxides, molybdenum oxides, tungsten oxides, and mixed oxides or composite oxides thereof. Particularly preferably, the first inorganic oxide is alumina, ceria, or a magnesia/alumina composite oxide. One especially preferred inorganic oxide is alumina.

[0031] The first inorganic oxide may be a support material for the one or more platinum group metals, and/or for the first ceria-containing material.

[0032] Preferred first inorganic oxides preferably have a surface area in the range 10 to 1500 m.sup.2/g, pore volumes in the range 0.1 to 4 mL/g, and pore diameters from about 10 to 1000 Angstroms. High surface area inorganic oxides having a surface area greater than 80 m.sup.2/g are particularly preferred, e.g. high surface area ceria or alumina. Other preferred first inorganic oxides include magnesia/alumina composite oxides, optionally further comprising a cerium-containing component, e.g. ceria. In such cases the ceria may be present on the surface of the magnesia/alumina composite oxide, e.g. as a coating.

[0033] The one or more noble metals is preferably selected from the group consisting of palladium, platinum, rhodium, silver, gold, and mixtures thereof. Particularly preferably, the one or more noble metals is a mixture or alloy of platinum and palladium, preferably wherein the ratio of platinum to palladium is from 2:1 to 10:1 on a w/w basis, especially preferably about 5:1 on a w/w basis.

[0034] Preferably the one or more noble metals do not comprise or consist of rhodium. In other words, the second layer is preferably substantially free of rhodium. In some embodiments therefore the first layer and the second layer are preferably substantially free of rhodium. This may be advantageous as rhodium can negatively affect the catalytic activity of other catalytic metals, such as platinum, palladium, or mixtures and/or alloys thereof.

[0035] The one or more noble metals are generally in contact with the second ceria-containing material. Preferably the one or more noble metals are supported on the second ceria-containing material. In addition to, or alternatively to, being in contact with the second ceria-containing material, the one or more noble metals may be in contact with second inorganic oxide.

[0036] The second inorganic oxide is preferably an oxide of Groups 2, 3, 4, 5, 13 and 14 elements The second inorganic oxide is preferably selected from the group consisting of alumina, ceria, magnesia, silica, titania, zirconia, niobia, tantalum oxides, molybdenum oxides, tungsten oxides, and mixed oxides or composite oxides thereof. Particularly preferably, the second inorganic oxide is alumina, ceria, or a magnesia/alumina composite oxide. One especially preferred second inorganic oxide is alumina, e.g. a lanthanum-doped alumina.

[0037] The second inorganic oxide may be a support material for the one or more noble metals.

[0038] Preferred second inorganic oxides preferably have a surface area in the range 10 to 1500 m.sup.2/g, pore volumes in the range 0.1 to 4 mL/g, and pore diameters from about 10 to 1000 Angstroms. High surface area inorganic oxides having a surface area greater than 80 m.sup.2/g are particularly preferred, e.g. high surface area ceria or alumina. Other preferred second inorganic oxides include magnesia/alumina composite oxides, optionally further comprising a cerium-containing component, e.g. ceria. In such cases the ceria may be present on the surface of the magnesia/alumina composite oxide, e.g. as a coating.

[0039] The second ceria-containing material is preferably selected from the group consisting of cerium oxide, a ceria-zirconia mixed oxide, and an alumina-ceria-zirconia mixed oxide. Preferably the second ceria-containing material comprises bulk ceria. The second ceria-containing material may function as an oxygen storage material. Alternatively, or in addition, the second ceria-containing material may function as a NO.sub.x storage material, and/or as a support material for the one or more noble metals.

[0040] The second layer may function as an oxidation layer, e.g. a diesel oxidation catalyst layer suitable for the oxidation of hydrocarbons to CO.sub.2 and/or CO, and/or suitable for the oxidation of NO to NO.sub.2.

[0041] In some preferred lean NO.sub.x trap catalysts of the invention, the total loading of the one or more platinum group metals in the first layer is lower than the total loading of the one or more noble metals in the second layer. In such catalysts, preferably the ratio of the total loading of the one or more noble metals in the second layer to the total loading of the one or more platinum group metals in the first layer is at least 2:1 on a w/w basis.

[0042] In further preferred lean NO.sub.x trap catalysts of the invention, the total loading of the first ceria-containing material is greater than the total loading of the second ceria-containing material. In such catalysts, preferably the ratio of the total loading of the first ceria-containing material is greater than the total loading of the second ceria-containing material by at least 2:1 on a w/w basis, preferably at least 3:1 on a w/w basis, more preferably at least 5:1 on a w/w basis, particularly preferably at least 7:1 on a w/w basis.

[0043] It has surprisingly been found that lean NO.sub.x trap catalysts in which the total loading of the one or more platinum group metals in the first layer is lower than the total loading of the one or more noble metals in the second layer, and/or the total loading of the first ceria-containing material is greater than the total loading of the second ceria-containing material, have improved catalytic performance. Such catalysts have been found to show greater NO.sub.x storage properties and CO oxidation activity compared to lean NO.sub.x trap catalysts of the art.

[0044] It has further surprisingly been found that lean NO.sub.x trap catalysts as described herein in which a ceria-containing material, e.g. ceria, is present in the second layer, have improved performance relative to an equivalent catalyst that does not contain a ceria-containing material in the second layer. This finding is particularly surprising in that it is expected that the presence of a ceria-containing material, e.g. ceria, in the second layer would lead to a decrease in the oxidation of NO to NO.sub.2, as ceria would be expected to catalyst the reverse reaction, i.e. reduce NO.sub.2). The inventors have surprisingly found, however, that contrary to this expectation that lean NO.sub.x trap catalysts as described herein demonstrate this improved performance under both lean and rich conditions.

[0045] Without wishing to be bound by theory, it is thought that the arrangement described above, in which the relative loading of the one or more platinum group metals in the first layer is lower than that of the one or more noble metals in the second layer, and/or in which the relative loading of the first ceria-containing material (i.e. in the first layer) is higher than that of the second ceria-containing material (i.e. in the second layer), produces a separation of the NOx storage and oxidation functions of the lean NOx trap catalyst into separate layers. In doing so, there is a synergistic benefit in which the separated functions each individually have increased performance relative to an equivalent catalyst in which oxidation and NOx storage functions are located within the same layer.

[0046] In preferred lean NO.sub.x trap catalysts of the invention, the rare earth dopant comprises one or more of scandium, yttrium, lanthanum, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, or metal oxides thereof. Preferably the rare earth dopant comprises lanthanum, neodymium, or metal oxides thereof. Particularly preferably the rare earth dopant comprises lanthanum, e.g. consists essentially of lanthanum or consists of lanthanum.

[0047] In preferred catalysts of the invention, the first layer is substantially free of barium. Particularly preferred catalysts are those which are substantially free of barium, i.e. the first layer, second layer, and any additional layers are substantially free of barium. Particularly preferred first layers, second layers, additional layers, and lean NOx trap catalysts are also substantially free of alkali metals, e.g. potassium (K) and sodium (Na).

[0048] Some catalysts of the invention are therefore barium-free NO.sub.x trap catalysts comprising a first ceria-containing material or a first inorganic oxide comprising a rare earth dopant. In such catalysts, the first ceria-containing material or a first inorganic oxide comprising a rare earth dopant may function as a NO.sub.x storage material.

[0049] Catalysts of the invention that are substantially free of barium, or do not comprise barium as a NO.sub.x storage material (e.g. barium-free lean NO.sub.x trap catalysts), may be particularly advantageous because they store less NO.sub.x at temperatures in excess of 180, 200, 250 or 300° C., preferably about 300° C. than a comparable barium-containing catalyst. In other words, catalysts of the invention that are substantially free of barium, or do not comprise barium as a NO.sub.x storage material, have improved NO.sub.x release properties at temperatures in excess of 180, 200, 250 or 300° C., preferably about 300° C. than a comparable barium-containing catalyst. Such catalysts may also have improved sulfur tolerance relative to an equivalent barium-containing catalyst. In this context, “improved sulfur tolerance” means that catalysts of the invention that are substantially free of barium are either more resistant to sulfation, can be thermally desulfated at a lower temperature, or both, compared to an equivalent barium-containing catalyst.

[0050] The lean NO.sub.x trap catalysts of the invention may comprise further components that are known to the skilled person. For example, the compositions of the invention may further comprise at least one binder and/or at least one surfactant. Where a binder is present, dispersible alumina binders are preferred.

[0051] The lean NO.sub.x trap catalysts of the invention may preferably further comprise a metal or ceramic substrate having an axial length L. Preferably the substrate is a flow-through monolith or a filter monolith, but is preferably a flow-through monolith substrate.

[0052] The flow-through monolith substrate has a first face and a second face defining a longitudinal direction therebetween. The flow-through monolith substrate has a plurality of channels extending between the first face and the second face. The plurality of channels extend in the longitudinal direction and provide a plurality of inner surfaces (e.g. the surfaces of the walls defining each channel). Each of the plurality of channels has an opening at the first face and an opening at the second face. For the avoidance of doubt, the flow-through monolith substrate is not a wall flow filter.

[0053] The first face is typically at an inlet end of the substrate and the second face is at an outlet end of the substrate.

[0054] The channels may be of a constant width and each plurality of channels may have a uniform channel width.

[0055] Preferably within a plane orthogonal to the longitudinal direction, the monolith substrate has from 100 to 500 channels per square inch, preferably from 200 to 400. For example, on the first face, the density of open first channels and closed second channels is from 200 to 400 channels per square inch. The channels can have cross sections that are rectangular, square, circular, oval, triangular, hexagonal, or other polygonal shapes.

[0056] The monolith substrate acts as a support for holding catalytic material. Suitable materials for forming the monolith substrate include ceramic-like materials such as cordierite, silicon carbide, silicon nitride, zirconia, mullite, spodumene, alumina-silica magnesia or zirconium silicate, or of porous, refractory metal. Such materials and their use in the manufacture of porous monolith substrates is well known in the art.

[0057] It should be noted that the flow-through monolith substrate described herein is a single component (i.e. a single brick). Nonetheless, when forming an emission treatment system, the monolith used may be formed by adhering together a plurality of channels or by adhering together a plurality of smaller monoliths as described herein. Such techniques are well known in the art, as well as suitable casings and configurations of the emission treatment system.

[0058] In embodiments wherein the lean NO.sub.x trap catalyst comprises a ceramic substrate, the ceramic substrate may be made of any suitable refractory material, e.g., alumina, silica, titania, ceria, zirconia, magnesia, zeolites, silicon nitride, silicon carbide, zirconium silicates, magnesium silicates, aluminosilicates and metallo aluminosilicates (such as cordierite and spodumene), or a mixture or mixed oxide of any two or more thereof. Cordierite, a magnesium aluminosilicate, and silicon carbide are particularly preferred.

[0059] In embodiments wherein the lean NO.sub.x trap catalyst comprises a metallic substrate, the metallic substrate may be made of any suitable metal, and in particular heat-resistant metals and metal alloys such as titanium and stainless steel as well as ferritic alloys containing iron, nickel, chromium, and/or aluminium in addition to other trace metals.

[0060] The lean NO.sub.x trap catalysts of the invention may be prepared by any suitable means. For example, the first layer may be prepared by mixing the one or more platinum group metals, a first ceria-containing material, and a first inorganic oxide in any order. The manner and order of addition is not considered to be particularly critical. For example, each of the components of the first layer may be added to any other component or components simultaneously, or may be added sequentially in any order. Each of the components of the first layer may be added to any other component of the first layer by impregnation, adsorption, ion-exchange, incipient wetness, precipitation, or the like, or by any other means commonly known in the art.

[0061] The second layer may be prepared by mixing the one or more noble metals, a second ceria-containing material, and a second inorganic oxide in any order. The manner and order of addition is not considered to be particularly critical. For example, each of the components of the second layer may be added to any other component or components simultaneously, or may be added sequentially in any order. Each of the components of the second layer may be added to any other component of the second layer by impregnation, adsorption, ion-exchange, incipient wetness, precipitation, or the like, or by any other means commonly known in the art.

[0062] Preferably, the lean NO.sub.x trap catalyst as hereinbefore described is prepared by depositing the lean NO.sub.x trap catalyst on the substrate using washcoat procedures. A representative process for preparing the lean NO.sub.x trap catalyst using a washcoat procedure is set forth below. It will be understood that the process below can be varied according to different embodiments of the invention.

[0063] The washcoating is preferably performed by first slurrying finely divided particles of the components of the lean NO.sub.x trap catalyst as hereinbefore defined in an appropriate solvent, preferably water, to form a slurry. The slurry preferably contains between 5 to 70 weight percent solids, more preferably between 10 to 50 weight percent. Preferably, the particles are milled or subject to another comminution process in order to ensure that substantially all of the solid particles have a particle size of less than 20 microns in an average diameter, prior to forming the slurry. Additional components, such as stabilizers, binders, surfactants or promoters, may also be incorporated in the slurry as a mixture of water soluble or water-dispersible compounds or complexes.

[0064] The substrate may then be coated one or more times with the slurry such that there will be deposited on the substrate the desired loading of the lean NO.sub.x trap catalyst.

[0065] Preferably the first layer is supported/deposited directly on the metal or ceramic substrate. By “directly on” it is meant that there are no intervening or underlying layers present between the first layer and the metal or ceramic substrate.

[0066] Preferably the second layer is deposited on the first layer. Particularly preferably the second layer is deposited directly on the first layer. By “directly on” it is meant that there are no intervening or underlying layers present between the second layer and the first layer.

[0067] Thus in a preferred lean NO.sub.x trap catalyst of the invention, the first layer is deposited directly on the metal or ceramic substrate, and the second layer is deposited on the first layer.

[0068] Preferably the first layer and/or second layer are deposited on at least 60% of the axial length L of the substrate, more preferably on at least 70% of the axial length L of the substrate, and particularly preferably on at least 80% of the axial length L of the substrate.

[0069] In particularly preferred lean NO.sub.x trap catalysts of the invention, the first layer and the second layer are deposited on at least 80%, preferably at least 95%, of the axial length L of the substrate.

[0070] Preferably, the lean NO.sub.x trap catalyst comprises a substrate and at least one layer on the substrate. Preferably, the at least one layer comprises the first layer as hereinbefore described. This can be produced by the washcoat procedure described above. One or more additional layers may be added to the one layer of NO.sub.x adsorber catalyst composition, such as, but not limited to, the second layer as hereinbefore described.

[0071] In embodiments wherein one or more additional layers are present in addition to the first layer and the second layer as hereinbefore described, the one or more additional layers have a different composition to the first layer and the second layer as hereinbefore described

[0072] The one or more additional layers may comprise one zone or a plurality of zones, e.g. two or more zones. Where the one or more additional layers comprise a plurality of zones, the zones are preferably longitudinal zones. The plurality of zones, or each individual zone, may also be present as a gradient, i.e. a zone may not be of a uniform thickness along its entire length, to form a gradient. Alternatively a zone may be of uniform thickness along its entire length.

[0073] In some preferred embodiments, one additional layer, i.e. a first additional layer, is present.

[0074] Typically, the first additional layer comprises a platinum group metal (PGM) (referred to below as the “second platinum group metal”). It is generally preferred that the first additional layer comprises the second platinum group metal (PGM) as the only platinum group metal (i.e. there are no other PGM components present in the catalytic material, except for those specified).

[0075] The second PGM may be selected from the group consisting of platinum, palladium, and a combination or mixture of platinum (Pt) and palladium (Pd). Preferably, the platinum group metal is selected from the group consisting of palladium (Pd) and a combination or a mixture of platinum (Pt) and palladium (Pd). More preferably, the platinum group metal is selected from the group consisting of a combination or a mixture of platinum (Pt) and palladium (Pd).

[0076] It is generally preferred that the first additional layer is (i.e. is formulated) for the oxidation of carbon monoxide (CO) and/or hydrocarbons (HCs).

[0077] Preferably, the first additional layer comprises palladium (Pd) and optionally platinum (Pt) in a ratio by weight of 1:0 (e.g. Pd only) to 1:4 (this is equivalent to a ratio by weight of Pt:Pd of 4:1 to 0:1). More preferably, the second layer comprises platinum (Pt) and palladium (Pd) in a ratio by weight of <4:1, such as ≤3.5:1.

[0078] When the platinum group metal is a combination or mixture of platinum and palladium, then the first additional layer comprises platinum (Pt) and palladium (Pd) in a ratio by weight of 5:1 to 3.5:1, preferably 2.5:1 to 1:2.5, more preferably 1:1 to 2:1.

[0079] The first additional layer typically further comprises a support material (referred to herein below as the “second support material”). The second PGM is generally disposed or supported on the second support material.

[0080] The second support material is preferably a refractory oxide. It is preferred that the refractory oxide is selected from the group consisting of alumina, silica, ceria, silica alumina, ceria-alumina, ceria-zirconia and alumina-magnesium oxide. More preferably, the refractory oxide is selected from the group consisting of alumina, ceria, silica-alumina and ceria-zirconia. Even more preferably, the refractory oxide is alumina or silica-alumina, particularly silica-alumina.

[0081] A particularly preferred first additional layer comprises a silica-alumina support, platinum, palladium, barium, a molecular sieve, and a platinum group metal (PGM) on an alumina support, e.g. a rare earth-stabilised alumina. Particularly preferably, this preferred first additional layer comprises a first zone comprising a silica-alumina support, platinum, palladium, barium, a molecular sieve, and a second zone comprising a platinum group metal (PGM) on an alumina support, e.g. a rare earth-stabilised alumina. This preferred first additional layer may have activity as an oxidation catalyst, e.g. as a diesel oxidation catalyst (DOC).

[0082] A further preferred first additional layer comprises, consists of, or consists essentially of a platinum group metal on alumina. This preferred second layer may have activity as an oxidation catalyst, e.g. as a NO.sub.2-maker catalyst.

[0083] A further preferred first additional layer comprises a platinum group metal, rhodium, and a cerium-containing component.

[0084] In other preferred embodiments, more than one of the preferred first additional layers described above are present, in addition to the lean NO.sub.x trap catalyst. In such embodiments, the one or more additional layers may be present in any configuration, including zoned configurations.

[0085] Preferably the first additional layer is disposed or supported on the lean NO.sub.x trap catalyst.

[0086] The first additional layer may, additionally or alternatively, be disposed or supported on the substrate (e.g. the plurality of inner surfaces of the through-flow monolith substrate).

[0087] The first additional layer may be disposed or supported on the entire length of the substrate or the lean NO.sub.x trap catalyst. Alternatively the first additional layer may be disposed or supported on a portion, e.g. 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, 90%, or 95%, of the substrate or the lean NO.sub.x trap catalyst.

[0088] Alternatively, the first layer, and/or second layer may be extruded to form a flow-through or filter substrate. In such cases the lean NOx trap catalyst is an extruded lean NO.sub.x trap catalyst comprising the first layer, and/or second layer as hereinbefore described.

[0089] A further aspect of the invention is an emission treatment system for treating a flow of a combustion exhaust gas comprising the lean NO.sub.x trap catalyst as hereinbefore defined. In preferred systems, the internal combustion engine is a diesel engine, preferably a light duty diesel engine. The lean NO.sub.x trap catalyst may be placed in a close-coupled position or in the underfloor position.

[0090] The emission treatment system typically further comprises an emissions control device.

[0091] The emissions control devices is preferably downstream of the lean NO.sub.x trap catalyst.

[0092] Examples of an emissions control device include a diesel particulate filter (DPF), a lean NO.sub.x trap (LNT), a lean NO.sub.x catalyst (LNC), a selective catalytic reduction (SCR) catalyst, a diesel oxidation catalyst (DOC), a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, an ammonia slip catalyst (ASC), a cold start catalyst (dCSC™) and combinations of two or more thereof. Such emissions control devices are all well known in the art.

[0093] Some of the aforementioned emissions control devices have filtering substrates. An emissions control device having a filtering substrate may be selected from the group consisting of a diesel particulate filter (DPF), a catalysed soot filter (CSF), and a selective catalytic reduction filter (SCRF™) catalyst.

[0094] It is preferred that the emission treatment system comprises an emissions control device selected from the group consisting of a lean NO.sub.x trap (LNT), an ammonia slip catalyst (ASC), diesel particulate filter (DPF), a selective catalytic reduction (SCR) catalyst, a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, and combinations of two or more thereof. More preferably, the emissions control device is selected from the group consisting of a diesel particulate filter (DPF), a selective catalytic reduction (SCR) catalyst, a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, and combinations of two or more thereof. Even more preferably, the emissions control device is a selective catalytic reduction (SCR) catalyst or a selective catalytic reduction filter (SCRF™) catalyst.

[0095] When the emission treatment system of the invention comprises an SCR catalyst or an SCRF™ catalyst, then the emission treatment system may further comprise an injector for injecting a nitrogenous reductant, such as ammonia, or an ammonia precursor, such as urea or ammonium formate, preferably urea, into exhaust gas downstream of the lean NO.sub.x trap catalyst and upstream of the SCR catalyst or the SCRF™ catalyst.

[0096] Such an injector may be fluidly linked to a source (e.g. a tank) of a nitrogenous reductant precursor. Valve-controlled dosing of the precursor into the exhaust gas may be regulated by suitably programmed engine management means and closed loop or open loop feedback provided by sensors monitoring the composition of the exhaust gas.

[0097] Ammonia can also be generated by heating ammonium carbamate (a solid) and the ammonia generated can be injected into the exhaust gas.

[0098] Alternatively or in addition to the injector, ammonia can be generated in situ (e.g. during rich regeneration of a LNT disposed upstream of the SCR catalyst or the SCRF™ catalyst, e.g. a lean NO.sub.x trap catalyst of the invention). Thus, the emission treatment system may further comprise an engine management means for enriching the exhaust gas with hydrocarbons.

[0099] The SCR catalyst or the SCRF™ catalyst may comprise a metal selected from the group consisting of at least one of Cu, Hf, La, Au, In, V, lanthanides and Group VIII transition metals (e.g. Fe), wherein the metal is supported on a refractory oxide or molecular sieve. The metal is preferably selected from Ce, Fe, Cu and combinations of any two or more thereof, more preferably the metal is Fe or Cu.

[0100] The refractory oxide for the SCR catalyst or the SCRF™ catalyst may be selected from the group consisting of Al.sub.2O.sub.3, TiO.sub.2, CeO.sub.2, SiO.sub.2, ZrO.sub.2 and mixed oxides containing two or more thereof. The non-zeolite catalyst can also include tungsten oxide (e.g. V.sub.2O.sub.5/WO.sub.3/TiO.sub.2, WO.sub.x/CeZr.sub.2, WO.sub.x/ZrO.sub.2 or Fe/WO.sub.x/ZrO.sub.2).

[0101] It is particularly preferred when an SCR catalyst, an SCRF™ catalyst or a washcoat thereof comprises at least one molecular sieve, such as an aluminosilicate zeolite or a SAPO. The at least one molecular sieve can be a small, a medium or a large pore molecular sieve. By “small pore molecular sieve” herein we mean molecular sieves containing a maximum ring size of 8, such as CHA; by “medium pore molecular sieve” herein we mean a molecular sieve containing a maximum ring size of 10, such as ZSM-5; and by “large pore molecular sieve” herein we mean a molecular sieve having a maximum ring size of 12, such as beta. Small pore molecular sieves are potentially advantageous for use in SCR catalysts.

[0102] In the emission treatment system of the invention, preferred molecular sieves for an SCR catalyst or an SCRF™ catalyst are synthetic aluminosilicate zeolite molecular sieves selected from the group consisting of AEI, ZSM-5, ZSM-20, ERI including ZSM-34, mordenite, ferrierite, BEA including Beta, Y, CHA, LEV including Nu-3, MCM-22 and EU-1, preferably AEI or CHA, and having a silica-to-alumina ratio of about 10 to about 50, such as about 15 to about 40.

[0103] In a first emission treatment system embodiment, the emission treatment system comprises the lean NO.sub.x trap catalyst of the invention and a catalysed soot filter (CSF). The lean NO.sub.x trap catalyst is typically followed by (e.g. is upstream of) the catalysed soot filter (CSF). Thus, for example, an outlet of the lean NO.sub.x trap catalyst is connected to an inlet of the catalysed soot filter.

[0104] A second emission treatment system embodiment relates to an emission treatment system comprising the lean NO.sub.x trap catalyst of the invention, a catalysed soot filter (CSF) and a selective catalytic reduction (SCR) catalyst.

[0105] The lean NO.sub.x trap catalyst is typically followed by (e.g. is upstream of) the catalysed soot filter (CSF). The catalysed soot filter is typically followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. A nitrogenous reductant injector may be arranged between the catalysed soot filter (CSF) and the selective catalytic reduction (SCR) catalyst. Thus, the catalysed soot filter (CSF) may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst.

[0106] In a third emission treatment system embodiment, the emission treatment system comprises the lean NO.sub.x trap catalyst of the invention, a selective catalytic reduction (SCR) catalyst and either a catalysed soot filter (CSF) or a diesel particulate filter (DPF).

[0107] In the third emission treatment system embodiment, the lean NO.sub.x trap catalyst of the invention is typically followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. A nitrogenous reductant injector may be arranged between the oxidation catalyst and the selective catalytic reduction (SCR) catalyst. Thus, the catalyzed monolith substrate may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. The selective catalytic reduction (SCR) catalyst are followed by (e.g. are upstream of) the catalysed soot filter (CSF) or the diesel particulate filter (DPF).

[0108] A fourth emission treatment system embodiment comprises the lean NO.sub.x trap catalyst of the invention and a selective catalytic reduction filter (SCRF™) catalyst. The lean NO.sub.x trap catalyst of the invention is typically followed by (e.g. is upstream of) the selective catalytic reduction filter (SCRF™) catalyst.

[0109] A nitrogenous reductant injector may be arranged between the lean NO.sub.x trap catalyst and the selective catalytic reduction filter (SCRF™) catalyst. Thus, the lean NO.sub.x trap catalyst may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction filter (SCRF™) catalyst.

[0110] When the emission treatment system comprises a selective catalytic reduction (SCR) catalyst or a selective catalytic reduction filter (SCRF™) catalyst, such as in the second to fourth exhaust system embodiments described hereinabove, an ASC can be disposed downstream from the SCR catalyst or the SCRF™ catalyst (i.e. as a separate monolith substrate), or more preferably a zone on a downstream or trailing end of the monolith substrate comprising the SCR catalyst can be used as a support for the ASC.

[0111] Another aspect of the invention relates to a vehicle. The vehicle comprises an internal combustion engine, preferably a diesel engine. The internal combustion engine preferably the diesel engine, is coupled to an emission treatment system of the invention.

[0112] It is preferred that the diesel engine is configured or adapted to run on fuel, preferably diesel fuel, comprising 50 ppm of sulfur, more preferably ≤15 ppm of sulfur, such as 10 ppm of sulfur, and even more preferably ≤5 ppm of sulfur.

[0113] The vehicle may be a light-duty diesel vehicle (LDV), such as defined in US or European legislation. A light-duty diesel vehicle typically has a weight of <2840 kg, more preferably a weight of <2610 kg. In the US, a light-duty diesel vehicle (LDV) refers to a diesel vehicle having a gross weight of ≤8,500 pounds (US lbs). In Europe, the term light-duty diesel vehicle (LDV) refers to (i) passenger vehicles comprising no more than eight seats in addition to the driver's seat and having a maximum mass not exceeding 5 tonnes, and (ii) vehicles for the carriage of goods having a maximum mass not exceeding 12 tonnes.

[0114] Alternatively, the vehicle may be a heavy-duty diesel vehicle (HDV), such as a diesel vehicle having a gross weight of >8,500 pounds (US lbs), as defined in US legislation.

[0115] A further aspect of the invention is a method of treating an exhaust gas from an internal combustion engine comprising contacting the exhaust gas with the lean NO.sub.x trap catalyst as hereinbefore described or the emission treatment system as hereinbefore described. In preferred methods, the exhaust gas is a rich gas mixture. In further preferred methods, the exhaust gas cycles between a rich gas mixture and a lean gas mixture.

[0116] In some preferred methods of treating an exhaust gas from an internal combustion engine, the exhaust gas is at a temperature of about 150to 300° C.

[0117] In further preferred methods of treating an exhaust gas from an internal combustion engine, the exhaust gas is contacted with one or more further emissions control devices, in addition to the lean NO.sub.x trap catalyst as hereinbefore described. The emissions control device or devices is preferably downstream of the lean NO.sub.x trap catalyst.

[0118] Examples of a further emissions control device include a diesel particulate filter (DPF), a lean NO.sub.x trap (LNT), a lean NO.sub.x catalyst (LNC), a selective catalytic reduction (SCR) catalyst, a diesel oxidation catalyst (DOC), a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, an ammonia slip catalyst (ASC), a cold start catalyst (dCSC) and combinations of two or more thereof. Such emissions control devices are all well known in the art.

[0119] Some of the aforementioned emissions control devices have filtering substrates. An emissions control device having a filtering substrate may be selected from the group consisting of a diesel particulate filter (DPF), a catalysed soot filter (CSF), and a selective catalytic reduction filter (SCRF™) catalyst.

[0120] It is preferred that the method comprises contacting the exhaust gas with an emissions control device selected from the group consisting of a lean NO.sub.x trap (LNT), an ammonia slip catalyst (ASC), diesel particulate filter (DPF), a selective catalytic reduction (SCR) catalyst, a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, and combinations of two or more thereof. More preferably, the emissions control device is selected from the group consisting of a diesel particulate filter (DPF), a selective catalytic reduction (SCR) catalyst, a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, and combinations of two or more thereof. Even more preferably, the emissions control device is a selective catalytic reduction (SCR) catalyst or a selective catalytic reduction filter (SCRF™) catalyst.

[0121] When the method of the invention comprises contacting the exhaust gas with an SCR catalyst or an SCRF™ catalyst, then the method may further comprise the injection of a nitrogenous reductant, such as ammonia, or an ammonia precursor, such as urea or ammonium formate, preferably urea, into exhaust gas downstream of the lean NO.sub.x trap catalyst and upstream of the SCR catalyst or the SCRF™ catalyst.

[0122] Such an injection may be carried out by an injector. The injector may be fluidly linked to a source (e.g. a tank) of a nitrogenous reductant precursor. Valve-controlled dosing of the precursor into the exhaust gas may be regulated by suitably programmed engine management means and closed loop or open loop feedback provided by sensors monitoring the composition of the exhaust gas.

[0123] Ammonia can also be generated by heating ammonium carbamate (a solid) and the ammonia generated can be injected into the exhaust gas.

[0124] Alternatively or in addition to the injector, ammonia can be generated in situ (e.g. during rich regeneration of a LNT disposed upstream of the SCR catalyst or the SCRF™ catalyst). Thus, the method may further comprise enriching of the exhaust gas with hydrocarbons.

[0125] The SCR catalyst or the SCRF™ catalyst may comprise a metal selected from the group consisting of at least one of Cu, Hf, La, Au, In, V, lanthanides and Group VIII transition metals (e.g. Fe), wherein the metal is supported on a refractory oxide or molecular sieve. The metal is preferably selected from Ce, Fe, Cu and combinations of any two or more thereof, more preferably the metal is Fe or Cu.

[0126] The refractory oxide for the SCR catalyst or the SCRF™ catalyst may be selected from the group consisting of Al.sub.2O.sub.3, TiO.sub.2, CeO.sub.2, SiO.sub.2, ZrO.sub.2 and mixed oxides containing two or more thereof. The non-zeolite catalyst can also include tungsten oxide (e.g. V.sub.2O.sub.5/WO.sub.3/TiO.sub.2, WO.sub.x/CeZrO.sub.2, WO.sub.x/ZrO.sub.2 or Fe/WO.sub.x/ZrO.sub.2).

[0127] It is particularly preferred when an SCR catalyst, an SCRF™ catalyst or a washcoat thereof comprises at least one molecular sieve, such as an aluminosilicate zeolite or a SAPO. The at least one molecular sieve can be a small, a medium or a large pore molecular sieve. By “small pore molecular sieve” herein we mean molecular sieves containing a maximum ring size of 8, such as CHA; by “medium pore molecular sieve” herein we mean a molecular sieve containing a maximum ring size of 10, such as ZSM-5; and by “large pore molecular sieve” herein we mean a molecular sieve having a maximum ring size of 12, such as beta. Small pore molecular sieves are potentially advantageous for use in SCR catalysts.

[0128] In the method of treating an exhaust gas of the invention, preferred molecular sieves for an SCR catalyst or an SCRF™ catalyst are synthetic aluminosilicate zeolite molecular sieves selected from the group consisting of AEI, ZSM-5, ZSM-20, ERI including ZSM-34, mordenite, ferrierite, BEA including Beta, Y, CHA, LEV including Nu-3, MCM-22 and EU-1, preferably AEI or CHA, and having a silica-to-alumina ratio of about 10 to about 50, such as about 15 to about 40.

[0129] In a first embodiment, the method comprises contacting the exhaust gas with the lean NO.sub.x trap catalyst of the invention and a catalysed soot filter (CSF). The lean NO.sub.x trap catalyst is typically followed by (e.g. is upstream of) the catalysed soot filter (CSF). Thus, for example, an outlet of the lean NO.sub.x trap catalyst is connected to an inlet of the catalysed soot filter.

[0130] A second embodiment of the method of treating an exhaust gas relates to a method comprising contacting the exhaust gas with the lean NO.sub.x trap catalyst of the invention, a catalysed soot filter (CSF) and a selective catalytic reduction (SCR) catalyst.

[0131] The lean NO.sub.x trap catalyst is typically followed by (e.g. is upstream of) the catalysed soot filter (CSF). The catalysed soot filter is typically followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. A nitrogenous reductant injector may be arranged between the catalysed soot filter (CSF) and the selective catalytic reduction (SCR) catalyst. Thus, the catalysed soot filter (CSF) may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst.

[0132] In a third embodiment of the method of treating an exhaust gas, the method comprises contacting the exhaust gas with the lean NO.sub.x trap catalyst of the invention, a selective catalytic reduction (SCR) catalyst and either a catalysed soot filter (CSF) or a diesel particulate filter (DPF).

[0133] In the third embodiment of the method of treating an exhaust gas, the lean NO.sub.x trap catalyst of the invention is typically followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. A nitrogenous reductant injector may be arranged between the oxidation catalyst and the selective catalytic reduction (SCR) catalyst. Thus, the lean NO.sub.x trap catalyst may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction (SCR) catalyst. The selective catalytic reduction (SCR) catalyst are followed by (e.g. are upstream of) the catalysed soot filter (CSF) or the diesel particulate filter (DPF).

[0134] A fourth embodiment of the method of treating an exhaust gas comprises the lean NO.sub.x trap catalyst of the invention and a selective catalytic reduction filter (SCRF™) catalyst. The lean NO.sub.x trap catalyst of the invention is typically followed by (e.g. is upstream of) the selective catalytic reduction filter (SCRF™) catalyst.

[0135] A nitrogenous reductant injector may be arranged between the lean NO.sub.x trap catalyst and the selective catalytic reduction filter (SCRF™) catalyst. Thus, the lean NO.sub.x trap catalyst may be followed by (e.g. is upstream of) a nitrogenous reductant injector, and the nitrogenous reductant injector may be followed by (e.g. is upstream of) the selective catalytic reduction filter (SCRF™) catalyst.

[0136] When the emission treatment system comprises a selective catalytic reduction (SCR) catalyst or a selective catalytic reduction filter (SCRF™) catalyst, such as in the second to fourth method embodiments described hereinabove, an ASC can be disposed downstream from the SCR catalyst or the SCRF™ catalyst (i.e. as a separate monolith substrate), or more preferably a zone on a downstream or trailing end of the monolith substrate comprising the SCR catalyst can be used as a support for the ASC.

EXAMPLES

[0137] The invention will now be illustrated by the following non-limiting examples.

[0138] Materials

[0139] All materials are commercially available and were obtained from known suppliers, unless noted otherwise.

[0140] General Preparation 1

[0141] Al.sub.2O.sub.2.CeO.sub.2.MgO—BaCO.sub.3 composite material was formed by impregnating Al.sub.2O.sub.3(56.14%).CeO.sub.2(6.52%).MgO(14.04%) with barium acetate and spray-drying the resultant slurry. This was followed by calcination at 650° C. for 1 hour. Target BaCO.sub.3 concentration is 23.3wt %.

[0142] General Preparation 2

[0143] 903 g La(NO.sub.3).sub.3 was dissolved in 3583 g demineralized water. 1850 g of a high surface area CeO.sub.2 was added in powder form and the mixture stirred for 60 minutes. The resulting slurry was spray-dried on a Spray Dryer in counter-current mode (two-fluid, fountain nozzle, with inlet temperature set at 300° C. and outlet 110° C.). The resulting powder was collected from the cyclone. The powder was calcined at 650° C. for 1 hour in a static oven.

[0144] Example Preparation

[0145] Preparation of [Al.sub.2O.sub.3.CeO.sub.2.MgO.Ba].Pt.Pd.CeO.sub.2—Composition A

[0146] 2.07 g/in.sup.3 [Al.sub.2O.sub.2.CeO.sub.2.MgO.BaCO.sub.3] (prepared according to general preparation 1 above) was made into a slurry with distilled water and then milled to reduce the average particle size (d.sub.90=13-15 μm). To the slurry, 30 g/ft.sup.3 Pt malonate and 6 g/ft.sup.3 Pd nitrate solution were added, and stirred until homogenous. The Pt/Pd was allowed to adsorb onto the support for 1 hour. To this slurry was added 2.1 g/in.sup.3 of pre-calcined CeO.sub.2 followed by 0.2 g/in.sup.3 alumina binder, and stirred until homogenous to form a washcoat.

[0147] Preparation of [Al.sub.2O.sub.3.LaO]Pt.Pd.CeO.sub.2—Composition B

[0148] Pt malonate (65 gft.sup.−3) and Pd nitrate (13 gft.sup.−3) were added to a slurry of [Al.sub.2O.sub.3(90.0%).LaO(4%)](1.2 gin.sup.−3) in water. The Pt and Pd were allowed to adsorb to the alumina support for 1 hour before CeO.sub.2 (0.3 gin.sup.−3) was added. The resultant slurry was made into a washcoat and thickened with natural thickener (hydroxyethylcellulose).

[0149] Preparation of [Al.sub.2O.sub.3.LaO]Pt.Pd—Composition C

[0150] Pt malonate (65 gft.sup.−3) and Pd nitrate (13 gft.sup.−3) were added to a slurry of [Al.sub.2O.sub.3(90.0%).LaO(4%)](1.2 gin.sup.−3) in water. The Pt and Pd were allowed to adsorb to the alumina support for 1 hour. The resultant slurry was made into a washcoat and thickened with natural thickener (hydroxyethylcellulose).

[0151] Preparation of [CeO.sub.2].Rh.Pt.Al.sub.2O.sub.3—Composition D

[0152] Rh nitrate (5 gft.sup.−3) was added to a slurry of CeO.sub.2 (0.4 gin.sup.−3) in water. Aqueous NH.sub.3 was added until pH 6.8 to promote Rh adsorbtion. Following this, Pt malonate (5 gft.sup.−3) was added to the slurry and allowed to adsorb to the support for 1 hour before alumina (boehmite, 0.2 gin.sup.−3) and binder (alumina, 0.1 gin.sup.−3) were added. The resultant slurry was made into a washcoat.

[0153] Catalyst 1

[0154] Each of washcoats A, C and D were coated sequentially onto a ceramic or metallic monolith using standard coating procedures, dried at 100° C. and calcined at 500° C. for 45 mins.

[0155] Catalyst 2

[0156] Each of washcoats A, B and D were coated sequentially onto a ceramic or metallic monolith using standard coating procedures, dried at 100° C. and calcined at 500° C. for 45 mins.

[0157] Catalyst 3—La 800 g/ft.sup.3

[0158] Preparation of Al.sub.2O.sub.3 PGM. [CeO.sub.2.La(13.1wt %)]

[0159] 1.2g/in.sup.3 Al.sub.2O.sub.3 is made into a slurry with distilled water and then milled to a d.sub.90 of 13-15 μm. To the slurry, 50 g/ft.sup.3 Pt malonate and 10 g/ft.sup.3 Pd nitrate solution is then added, and stirred until homogenous. The Pt/Pd is allowed to adsorb onto the support for 1 hour. To this is then added 3g/in.sup.3 of [CeO.sub.2.La(13.1 wt %)] (prepared according to general preparation 2 above) and 0.2 g/in.sup.3 alumina binder, and stirred until homogenous to form a washcoat. The washcoat is then coated onto a ceramic or metallic monolith using standard procedures, dried at 100° C. and calcined at 500° C. for 45 mins.

[0160] 0.75 g/in.sup.3 4% lanthanum-doped alumina is made into a slurry with distilled water and then milled to a d.sub.90 of 13-15 μm. To the slurry, 50 g/ft.sup.3 Pt malonate and 50 g/ft.sup.3 Pd nitrate solution is then added, and stirred until homogenous. The Pt/Pd is allowed to adsorb onto the support for 1 hour. To this is then added 0.75 g/in.sup.3 of high surface area Ce, and stirred until homogenous to form a washcoat. The washcoat is then coated onto a ceramic or metallic monolith using standard procedures, dried at 100° C. and calcined at 500° C. for 45 mins.

[0161] 0.4 g/in.sup.3 high surface area Ce is made into a slurry with distilled water. To the slurry, 5 g/ft.sup.3 Rh nitrate and 5 g/ft.sup.3 Pt malonate solution is then added, and stirred until homogenous. The Rh/Pt is allowed to adsorb onto the support for 1 hour. To this is then added 0.3 g/in.sup.3 Al.sub.2O.sub.3 binder, and stirred until homogenous to form a washcoat. The washcoat is then coated onto a ceramic or metallic monolith using standard procedures, dried at 100° C. and calcined at 500° C. for 45 mins.

[0162] Experimental Results

[0163] Catalysts 1 and 2 were hydrothermally aged at 800° C. for 16 h, in a gas stream consisting of 10% H.sub.2O, 20% O.sub.2, and balance N.sub.2. They were performance tested over a steady-state emissions cycle (three cycles of 300 s lean and 10 s rich, with a target NO.sub.x exposure of 1 g) using a 1.6 litre bench mounted diesel engine. Emissions were measured pre- and post-catalyst.

Example 1

[0164] The NO.sub.x storage performance of the catalysts was assessed by measuring NO.sub.x storage efficiency as a function of NO.sub.x stored. The results from one representative cycle at 150° C., following a deactivating precondition, are shown in Table 1 below.

TABLE-US-00001 TABLE 1 NO.sub.x stored NO.sub.x storage efficiency (%) (g) Catalyst 1 Catalyst 2 0.1 92 96 0.2 87 92 0.3 79 84 0.4 67 73 0.5 53 58 0.6 39 43

[0165] It can be seen from the results in Table 1 that Catalyst 2, comprising a Ce-containing middle layer, has higher NO.sub.x storage efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

Example 2

[0166] The NO.sub.x storage performance of the catalysts was assessed by measuring NO.sub.x storage efficiency as a function of NO.sub.x stored. The results from one representative cycle at 150° C., following a more activating precondition than that of Example 1 above, are shown in Table 2 below.

TABLE-US-00002 TABLE 2 NO.sub.x stored NO.sub.x storage efficiency (%) (g) Catalyst 1 Catalyst 2 0.1 33 57 0.2 18 34 0.3 — 18 0.4 — — 0.5 — — 0.6 — —

[0167] It can be seen from the results in Table 2 that, similarly to in Example 1 above, Catalyst 2, comprising a Ce-containing middle layer, has higher NO.sub.x storage efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

Example 3

[0168] The NO.sub.x storage performance of the catalysts was assessed by measuring NO.sub.x storage efficiency as a function of NO.sub.x stored. The results from one representative cycle at 200° C., following a deactivating precondition, are shown in Table 1 below.

TABLE-US-00003 TABLE 3 NO.sub.x stored NOx storage efficiency (%) (g) Catalyst 1 Catalyst 2 0.1 94 95 0.2 89 91 0.3 85 89 0.4 81 86 0.5 77 83 0.6 73 80

[0169] It can be seen from the results in Table 3 that Catalyst 2, comprising a Ce-containing middle layer, has higher NO.sub.x storage efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

[0170] Example 4

[0171] The NO.sub.x storage performance of the catalysts was assessed by measuring NO.sub.x storage efficiency as a function of NO.sub.x stored. The results from one representative cycle at 200° C., following a deactivating precondition, are shown in Table 1 below.

TABLE-US-00004 TABLE 4 NO.sub.x stored NOx storage efficiency (%) (g) Catalyst 1 Catalyst 2 0.1 72 85 0.2 61 81 0.3 45 69 0.4 36 58 0.5 30 47 0.6 — 41

[0172] It can be seen from the results in Table 4 that Catalyst 2, comprising a Ce-containing middle layer, has higher NO.sub.x storage efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

Example 5

[0173] The CO oxidation performance of the catalysts was assessed by measuring CO conversion over time. The results from one representative cycle at 175° C., following an activating steady state test condition, are shown in Table 5 below.

TABLE-US-00005 TABLE 5 Time CO conversion efficiency (%) (s) Catalyst 1 Catalyst 2 75 12 17 100 20 36 125 70 90 150 96 98 175 99 99

[0174] It can be seen from the results in Table 5 that Catalyst 2, comprising a Ce-containing middle layer, has higher CO conversion efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

[0175] This is further demonstrated by the time taken to each 25% and 50% CO conversion efficiency at 175° C. for each catalyst. Catalyst 1 achieved 25% CO conversion efficiency after 108 s, and 50% CO conversion efficiency after 121 s. Catalyst 2 achieved 25% CO conversion efficiency after 85 s, and 50% CO conversion efficiency after 110 s. Catalyst 2 therefore achieves CO light-off sooner than Catalyst 1.

Example 6

[0176] The CO oxidation performance of the catalysts was assessed by measuring CO conversion over time. The results from one representative cycle at 200° C., following an activating steady state test condition, are shown in Table 6 below.

TABLE-US-00006 TABLE 6 Time CO conversion efficiency (%) (s) Catalyst 1 Catalyst 2 75 15 25 100 26 51 125 78 95 150 97 99 175 99 99

[0177] It can be seen from the results in Table 6 that Catalyst 2, comprising a Ce-containing middle layer, has higher CO conversion efficiency than Catalyst 1, which does not comprise a Ce-containing middle layer.

[0178] This is further demonstrated by the time taken to each 25% and 50% CO conversion efficiency at 200° C. for each catalyst. Catalyst 1 achieved 25% CO conversion efficiency after 97 s, and 50% CO conversion efficiency after 118 s. Catalyst 2 achieved 25% CO conversion efficiency after 76 s, and 50% CO conversion efficiency after 99 s. Catalyst 2 therefore achieves CO light-off sooner than Catalyst 1.

Example 7

[0179] Catalysts 2 and 3 were hydrothermally aged at 800° C. for 16 h, in a gas stream consisting of 10% H.sub.2O, 20% O.sub.2, and balance N.sub.2. They were performance tested over a steady-state emissions cycle (three cycles of 300 s lean and 10 s rich, with a target NO.sub.x exposure of 1 g) using a 1.6 litre bench mounted diesel engine. Emissions were measured pre- and post-catalyst.

[0180] The NO.sub.x storage performance of the catalysts was assessed by measuring NO.sub.x conversion as a function of temperature. The results from one representative cycle are shown in Table 7 below.

TABLE-US-00007 TABLE 7 Temperature NO.sub.x conversion (%) (° C.) Catalyst 2 Catalyst 3 150 8.7 9.3 175 19.4 27.6 200 30.9 40.1 250 56 58.3 300 75.9 69.9 400 62.8 36.2

[0181] It can be seen from the results shown in Table 7 above that Catalyst 3, wherein the first layer comprises a rare earth-containing component (i.e. CeO.sub.2—La), has superior low temperature (i.e. less than 250° C.) NOx conversion performance than Catalyst 2, which is a conventional barium-containing catalyst.